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JP3487754B2 - Deodorizing filter medium and method for producing the same - Google Patents
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JP3487754B2 - Deodorizing filter medium and method for producing the same - Google Patents

Deodorizing filter medium and method for producing the same

Info

Publication number
JP3487754B2
JP3487754B2 JP04621598A JP4621598A JP3487754B2 JP 3487754 B2 JP3487754 B2 JP 3487754B2 JP 04621598 A JP04621598 A JP 04621598A JP 4621598 A JP4621598 A JP 4621598A JP 3487754 B2 JP3487754 B2 JP 3487754B2
Authority
JP
Japan
Prior art keywords
resin
deodorizing
filter medium
deodorizing filter
hot
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP04621598A
Other languages
Japanese (ja)
Other versions
JPH11253720A (en
Inventor
隆博 横山
達郎 中村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Japan Vilene Co Ltd
Original Assignee
Japan Vilene Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Japan Vilene Co Ltd filed Critical Japan Vilene Co Ltd
Priority to JP04621598A priority Critical patent/JP3487754B2/en
Priority to KR10-1998-0020254A priority patent/KR100477525B1/en
Priority to EP98110035A priority patent/EP0882485B1/en
Priority to US09/088,776 priority patent/US6177069B1/en
Priority to DE69807583T priority patent/DE69807583T2/en
Publication of JPH11253720A publication Critical patent/JPH11253720A/en
Application granted granted Critical
Publication of JP3487754B2 publication Critical patent/JP3487754B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Filtering Materials (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、臭気成分で汚染
された流体を濾過して清浄化するための脱臭濾材に関
し、特に、脱臭性能と加工性とに優れた脱臭濾材とその
製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deodorizing filter medium for filtering and cleaning a fluid contaminated with an odor component, and more particularly to a deodorizing filter medium excellent in deodorizing performance and processability and a method for producing the same.

【0002】[0002]

【従来の技術】近年、生活環境に対する意識向上には目
を見張るものがあり、とりわけ、臭いに寄せられる関心
は極めて大きく、従前求められてきた有害物質の除去の
みならず、不快な臭気物質の除去も要求されている。こ
れら臭気成分を除去するため、様々な脱臭濾材が提案さ
れてきた。係る脱臭濾材の大半は、通気性を有するシー
ト状の部材に、例えば活性炭や種々の化学脱臭剤からな
る粒子(以下、包括的に脱臭粉粒体と称する)を固着す
るものである。従来知られている粉粒体固着技術とし
て、種々のバインダを用いて、不織布等の基布に脱臭粉
粒体を固着担持せしめる手法が広く行われてきた。しか
しながら、その多くは、脱臭粉粒体の表面をバインダが
被覆してしまうため、当該粉粒体が本来有する性能を低
下させてしまうという欠点を有していた。
2. Description of the Related Art In recent years, there has been a remarkable increase in awareness of the living environment, and in particular, there is a great deal of interest in odors. Removal is also required. Various deodorizing filter media have been proposed to remove these odorous components. Most of such deodorizing filter materials adhere particles (for example, collectively referred to as deodorizing powder particles) made of, for example, activated carbon or various chemical deodorizing agents to a sheet-like member having air permeability. As a conventionally known technique for adhering powdery particles, a method of fixing and carrying deodorant powdery particles on a base cloth such as a non-woven fabric using various binders has been widely used. However, many of them have a drawback that the surface of the deodorized powder or granules is coated with the binder, and the performance originally possessed by the powder or granules is deteriorated.

【0003】これに対して、例えば、特開平8−266
845号公報(以下、文献)に提案される技術では、1
0mmから1mmの目開きを有する網体に予めエマルジ
ョン型アクリル系粘着剤を付着させておき、この粘着剤
を介して脱臭粉粒体(吸着素材粒子)を固着する。この
技術では、当該公報に開示されるように、1mmから1
0mmの目開きを有する網体に粘着剤をスプレーやコー
ター等で塗布するものである。従って、所望の脱臭効率
を実現するために、例えば100μm以下といった目開
きの網体を選定しても、粘着剤塗布の段階で開口部分が
つぶれ、得られる濾材の圧力損失が高くなってしまう。
On the other hand, for example, Japanese Patent Application Laid-Open No. 8-266.
In the technique proposed in Japanese Patent Publication No. 845 (hereinafter referred to as “reference”), 1
An emulsion type acrylic pressure-sensitive adhesive is preliminarily attached to a mesh having a mesh size of 0 mm to 1 mm, and deodorant powder particles (adsorption material particles) are fixed via this pressure-sensitive adhesive. In this technique, as disclosed in the publication, 1 mm to 1
The pressure-sensitive adhesive is applied to a net having a 0 mm opening by a sprayer or a coater. Therefore, even if a mesh body having an opening of 100 μm or less is selected in order to achieve a desired deodorizing efficiency, the opening portion is crushed at the stage of applying the pressure-sensitive adhesive, and the pressure loss of the obtained filter medium becomes high.

【0004】また、他の粉粒体固着技術として、予め粒
状の熱可塑性樹脂から成る接着剤と脱臭粉粒体を混合
し、可撓性を有するシート状の支持材料の表面に塗布し
て濾材とする技術が知られている。通常、接着剤は脱臭
粉粒体の粒径よりも小さいものが使われるが、係る構造
の脱臭濾材では、脱臭粉粒体同士が結合剤粒子を介して
三次元的に点接着し、所定の厚さに立体構造を成して構
成せしめることが可能である。従って、前述の文献に開
示される技術に較べて、高密度で脱臭粉粒体を具えた脱
臭濾材を実現することができる。
As another technique for adhering powdery particles, a deodorizing powdery material is mixed with an adhesive made of a granular thermoplastic resin in advance, and the mixture is applied to the surface of a flexible sheet-shaped support material to obtain a filter medium. The technology to do is known. Usually, an adhesive having a particle size smaller than that of the deodorizing powder particles is used.However, in the deodorizing filter material having such a structure, the deodorizing powder particles are three-dimensionally point-bonded to each other through the binder particles, and a predetermined amount It is possible to form a three-dimensional structure in the thickness. Therefore, as compared with the technique disclosed in the above-mentioned document, it is possible to realize a deodorizing filter medium having a high density of deodorizing powder particles.

【0005】[0005]

【発明が解決しようとする課題】上述したように粒状の
接着剤を使用する技術では、予め脱臭粉粒体と結合剤粒
子とを混合し、これを支持材料に配置、固着させるもの
である。ここで、1つの脱臭粉粒体に着目すれば、結合
剤粒子の粒径や、当該粉粒体との相対的な組成比を選択
することによって、1つの脱臭粉粒体を固着する度合い
を制御することは可能である。しかしながら、結合剤粒
子は脱臭粉粒体を個々に独立した点で保持するに過ぎな
い。従って、周知のように、フィルタエレメントとして
折り加工を施し、高効率の脱臭濾材を実現するには機械
的強度に乏しく、脱臭粉粒体脱落を回避するために、上
記折り加工に際しての設計に制限を有するという問題点
があった。また、この点接着技術の場合、十分な固着を
図るためには接着剤を熱溶融させる必要があるが、熱処
理時に接着剤が流動化し、重力方向下側に接着剤が局在
化する傾向にある。これがため、熱処理条件が難しく、
接着剤による圧力損失が大きくなってしまう、若しく
は、流動化した接着剤で脱臭粉粒体が被覆されてしまう
といった問題が有った。
As described above, in the technique of using the granular adhesive, the deodorizing powder particles and the binder particles are mixed in advance, and the particles are arranged and fixed on the supporting material. Here, if one deodorizing powder is focused, the degree of fixing one deodorizing powder can be determined by selecting the particle size of the binder particles and the relative composition ratio with the powder. It is possible to control. However, the binder particles only hold the deodorant granules at individual points. Therefore, as is well known, the mechanical strength is poor in order to realize a highly efficient deodorizing filter material by performing folding processing as a filter element, and in order to avoid the deodorizing powder granules falling off, the design at the time of the folding processing is limited. There was a problem of having. In addition, in the case of this point bonding technique, it is necessary to heat-melt the adhesive in order to achieve sufficient fixation, but the adhesive tends to fluidize during heat treatment, and the adhesive tends to be localized on the lower side in the direction of gravity. is there. Therefore, heat treatment conditions are difficult,
There is a problem that the pressure loss due to the adhesive becomes large, or the deodorized powder particles are coated with the fluidized adhesive.

【0006】本願発明者らは、上述した従来の問題点に
鑑み、脱臭粉粒体を固着する構成成分が互いに連続した
状態で設けられることにより機械的強度に優れ、しか
も、脱臭粉粒体を高密度で具えた脱臭濾材を実現するた
めに鋭意検討した結果、本発明を創出するに至った。従
って、この発明の目的は、圧力損失が低く、脱臭効率が
高く、しかも機械的な強度に優れた、加工適性の高い脱
臭濾材を提供することにある。
In view of the above-mentioned conventional problems, the inventors of the present invention have excellent mechanical strength by providing the constituents for fixing the deodorant powder granules in a continuous state with each other. As a result of intensive studies to realize a deodorizing filter medium having a high density, the present invention has been created. Therefore, an object of the present invention is to provide a deodorizing filter medium having a low pressure loss, a high deodorizing efficiency, an excellent mechanical strength, and a high processability.

【0007】[0007]

【課題を解決するための手段】この目的の達成を図るた
め、本願の第一発明に係る脱臭濾材の構成によれば、ホ
ットメルト樹脂のみからなる連結部と樹脂凝集部で構成
されたウエブの一方の表面に、上述の樹脂凝集部を介し
て脱臭粉粒体を固着してなる積層単位を有し、前述した
ウエブの他方の表面と、他の積層単位を構成する脱臭粉
粒体とが樹脂凝集部を介して固着してなることを特徴と
している。
In order to achieve this object, according to the constitution of the deodorizing filter material according to the first invention of the present application, a web composed of a connecting portion made of only hot melt resin and a resin aggregating portion is provided. On one surface, it has a laminated unit formed by fixing the deodorant powder through the resin agglomerate part, the other surface of the above-mentioned web, and the deodorant powder constituting the other laminated unit. It is characterized in that it is adhered through the resin agglomeration part.

【0008】また、この出願の第二発明に係る脱臭濾材
の製造方法によれば、ホットメルト不織布の表面に脱臭
粉粒体を配した後、加熱処理によって上述のホットメル
ト不織布と前述の脱臭粉粒体とが接する部分に樹脂凝集
部を形成し、かつ、この樹脂凝集部と、ホットメルト樹
脂からなる連結部とで構成されたウエブを形成する第一
の工程と、前述した脱臭粉粒体のうち、前述のウエブに
固着された脱臭粉粒体のみを残存せしめて積層単位を形
成する第二の工程と、この積層単位に固着された前述の
脱臭粉粒体に接してホットメルト不織布を積層し、前述
した第一の工程と第二の工程とを順次行うことを特徴と
している。
Further, according to the method for producing a deodorizing filter medium according to the second invention of this application, after the deodorizing powder granules are arranged on the surface of the hot-melt nonwoven fabric, the hot-melt nonwoven fabric and the deodorizing powder are heated by heat treatment. A first step of forming a resin agglomerated portion in a portion in contact with the granules and forming a web composed of the resin agglomerated portion and a connecting portion made of a hot melt resin, and the deodorized powder granules described above. Of these, a second step of forming only a deodorizing powder granule fixed to the above-mentioned web to form a laminated unit, and a hot melt non-woven fabric in contact with the deodorizing powder granule fixed to this laminating unit. It is characterized in that the layers are laminated and the above-mentioned first step and second step are sequentially performed.

【0009】[0009]

【発明の実施の形態】まず、この出願の第一発明に係る
脱臭濾材の実施形態につき、図を参照して説明する。図
1は、本発明の濾材構成を模式的な断面により示す図で
ある。
BEST MODE FOR CARRYING OUT THE INVENTION First, an embodiment of a deodorizing filter medium according to the first invention of this application will be described with reference to the drawings. FIG. 1 is a schematic cross-sectional view showing the structure of the filter medium of the present invention.

【0010】本発明の脱臭濾材を構成するウエブ15
は、連結部11と樹脂凝集部13とからなり、何れも、
ホットメルト樹脂で構成される。この様な構成のウエブ
15は、第二発明に係る製造方法で言うホットメルト不
織布を脱臭粉粒体17の接触下で加熱処理することによ
り得られるものである(後段で詳述)。
Web 15 constituting the deodorizing filter material of the present invention
Is composed of a connecting portion 11 and a resin aggregating portion 13, and
Composed of hot melt resin. The web 15 having such a structure is obtained by heat-treating the hot-melt nonwoven fabric referred to in the manufacturing method according to the second aspect of the invention under the contact of the deodorizing powder granules 17 (detailed later).

【0011】このようなウエブが形成可能なホットメル
ト樹脂としては、熱可塑性ポリアミド系樹脂、熱可塑性
ポリエステル樹脂、熱可塑性ポリウレタン樹脂、ポリオ
レフィン樹脂、またはポリオレフィン変性樹脂などを、
各々、単独または混合して用いることができる。ここで
云うポリオレフィン変性樹脂としては、エチレン−酢酸
ビニル共重合体、エチレン−酢酸ビニル共重合体の鹸化
物、エチレン−エチルアクリレート共重合体、エチレン
−アクリル酸共重合体、エチレン−メタクリル酸共重合
体、エチレン−マレイン酸共重合体、アイオノマー樹脂
(エチレン−メタクリル酸共重合体に金属を付加した感
熱性樹脂)などが挙げられる。本発明並びに後段で詳述
する本願方法発明で利用できるホットメルト樹脂として
は、MIが50以上500以下のものを選択すればよ
い。この好適範囲よりも低いMIの樹脂は、加熱処理時
に流動性が低く、熱処理時に樹脂凝集部が形成されにく
く、脱臭粉粒体の固着が不完全となることがある。さら
に、上記範囲よりも高い樹脂では、加熱処理時の流動性
が高く、積層単位の形態保持が難しくなる。
As the hot-melt resin capable of forming such a web, a thermoplastic polyamide resin, a thermoplastic polyester resin, a thermoplastic polyurethane resin, a polyolefin resin, a polyolefin-modified resin, or the like can be used.
Each can be used alone or as a mixture. Examples of the polyolefin-modified resin referred to here include ethylene-vinyl acetate copolymer, saponified ethylene-vinyl acetate copolymer, ethylene-ethyl acrylate copolymer, ethylene-acrylic acid copolymer, ethylene-methacrylic acid copolymer. Combined, ethylene-maleic acid copolymer, ionomer resin
(A heat-sensitive resin obtained by adding a metal to an ethylene-methacrylic acid copolymer) and the like. As the hot melt resin that can be used in the present invention and the method invention of the present application described in detail later, one having MI of 50 or more and 500 or less may be selected. A resin having an MI lower than this preferable range has low fluidity during heat treatment, a resin agglomerate is less likely to be formed during heat treatment, and the deodorant powder granules may not be completely fixed. Further, if the resin content is higher than the above range, the fluidity at the time of heat treatment is high, and it becomes difficult to maintain the shape of the laminated unit.

【0012】また、脱臭粉粒体としては、従来知られて
いる活性炭やその他粒子状の化学脱臭剤を種々選択して
用いることが出来るが、高効率と低圧損とを実現するに
は当該粉粒体の平均粒径を0.147mm(100メッ
シュ)以上1.65mm(10メッシュ)以下とするの
が好適である。この好適範囲の下限よりも細かい平均粒
径の脱臭粉粒体を用いた場合には、初期の脱臭効率を高
く採れる反面、圧力損失が大きくなってしまう。
[0012] As the deodorizing powdery granules, conventionally known activated carbon and other particulate chemical deodorizing agents can be selected and used, but in order to realize high efficiency and low pressure loss The average particle size of the granules is preferably 0.147 mm (100 mesh) or more and 1.65 mm (10 mesh) or less. When a deodorizing powder having an average particle size smaller than the lower limit of this preferable range is used, the initial deodorizing efficiency can be made high, but the pressure loss becomes large.

【0013】さらに、上記好適範囲の上限よりも大きな
平均粒径の脱臭粉粒体を用いる場合には脱臭効率が低下
する傾向にある。本発明の脱臭濾材を構成する1つの積
層単位に担持される脱臭粉粒体の量は、概ね当該粉粒体
の平均粒径に応じ、比較的粒径が大きい場合には脱臭効
率が低くなるが、積層単位数を多く設計することによっ
て、脱臭濾材に要求される脱臭効率を達成することがで
きる。この際、各積層単位を構成する脱臭粉粒体の平均
粒径は、互いに異なっても良い。また、脱臭濾材の加工
適性、即ち、折り加工に必要な屈曲性や巻き取り時に必
要な可撓性などを考慮して、当該濾材の厚さは5mm以
下とするのが好ましく、好適には1〜4mm程度が良
い。
Further, when a deodorizing powder having an average particle size larger than the upper limit of the above-mentioned preferred range is used, the deodorizing efficiency tends to decrease. The amount of the deodorizing powder particles carried in one laminated unit constituting the deodorizing filter material of the present invention generally depends on the average particle size of the powder particles, and the deodorizing efficiency becomes low when the particle size is relatively large. However, by designing a large number of laminated units, the deodorizing efficiency required for the deodorizing filter medium can be achieved. At this time, the average particle diameters of the deodorant powder granules constituting each laminated unit may be different from each other. Further, in consideration of the processing suitability of the deodorizing filter medium, that is, the flexibility required for folding, the flexibility required for winding, etc., the thickness of the filter medium is preferably 5 mm or less, and preferably 1 mm. About 4 mm is good.

【0014】次いで、この出願の第二発明である製造方
法の実施形態につき説明する。既に述べたように、本方
法発明では、ホットメルト不織布を積層し、これに脱臭
粉粒体を接触配置した状態で加熱処理を行う構成として
いる。この際に用いるホットメルト不織布としては、前
述した種々の樹脂で構成され、面密度が10〜30g/
2のものが好適であり、特に、15〜25g/m2のも
のが好ましい。これら好適範囲よりも小さな面密度とし
た場合、不織布としての均一性に欠けるため、結果とし
て、積層単位に固着された脱臭粉粒体の均一性を損な
い、臭気物質のリークにより脱臭濾材の効率が低下す
る。また、上記好適範囲を超えても固着強度の向上は望
めず、脱臭濾材としての圧力損失のみ増大することとな
る。
Next, an embodiment of the manufacturing method which is the second invention of this application will be described. As described above, in the present invention, the hot-melt nonwoven fabric is laminated, and the heat treatment is performed in the state where the deodorized powder granules are placed in contact therewith. The hot melt nonwoven fabric used in this case is composed of the various resins described above and has an area density of 10 to 30 g /
m 2 is preferable, and 15 to 25 g / m 2 is particularly preferable. When the areal density is smaller than these preferable ranges, the non-woven fabric lacks uniformity, and as a result, the uniformity of the deodorizing powder particles fixed to the laminate unit is impaired, and the efficiency of the deodorizing filter medium is reduced due to the leakage of odorous substances. descend. Further, even if it exceeds the above-mentioned preferable range, the improvement of the fixing strength cannot be expected, and only the pressure loss as the deodorizing filter medium will increase.

【0015】さらに、本発明で用いるホットメルト不織
布の開口径は、得られる脱臭濾材に均一に脱臭粉粒体を
担持するために、所望とする当該粉粒体の粒径よりも小
さいことが望ましい。例えば、脱臭粉粒体の粒径を32
メッシュ(約500μm)程度とする場合、熱処理後の
ウエブ開口径が100μm以下となるように、前述のホ
ットメルト不織布を選択して用いるのが好適である。
Further, the opening diameter of the hot-melt nonwoven fabric used in the present invention is preferably smaller than the desired particle diameter of the powder or granular material in order to uniformly support the deodorizing powder or granular material on the obtained deodorizing filter material. . For example, the particle size of the deodorant powder is 32
When the mesh (about 500 μm) is used, it is preferable to select and use the above-mentioned hot melt nonwoven fabric so that the web opening diameter after heat treatment is 100 μm or less.

【0016】この方法発明では、ホットメルト不織布を
構成する繊維が加熱処理によって可塑化溶融し、その一
部は繊維径が細いため溶融切断されて脱臭粉粒体との接
点に集まり、樹脂凝集部を形成すると考えられる。この
点につき、図1に示す積層単位のうち、ウエブ15側か
ら1つの脱臭粉粒体17に着目して平面を示す図2を参
照して説明すれば、上述した樹脂凝集部13の形成と共
に、比較的繊維径が太いものにあっては可塑化溶融して
も切断を受けず、連結部11として強固な網状構造を構
成する。この加熱処理に当たっては、例えばカレンダ
ー、熱風ヒーター、赤外線ヒーター、水蒸気による加
熱、対向する1対の無端ベルト間に布帛を挟持して加熱
する装置など、従来知られている手段とすることが出来
る。このうち、熱量を持った流体で加熱処理を行うこと
によって、積層単位の厚さ方向にわたる連通孔(図1中
に矢印Aで示す)を形成することができる。さらに、特
に好適な態様として、熱可塑性ポリアミド系樹脂または
エチレン−酢酸ビニル共重合体樹脂からなるホットメル
ト不織布を用い、水蒸気による加熱処理を採用すること
により、当該樹脂が湿熱時に収縮切断し易い特性を持つ
ため、上記切断を効率的に行うことができる。また、ホ
ットメルト不織布の可塑化溶融に伴う強度低下を補う必
要がある場合には脱臭濾材の最外層を構成するホットメ
ルト不織布の支持体として、塵埃捕集用のフィルタ素材
を付加しても良い。
In this method invention, the fibers constituting the hot melt non-woven fabric are plasticized and melted by the heat treatment, and a part of the fibers are melted and cut due to the small fiber diameter and gathered at the contact point with the deodorized powder granules, and the resin agglomerated part Is thought to form. This point will be described with reference to FIG. 2 showing a plane focusing on one deodorant powder granule 17 from the web 15 side in the laminated unit shown in FIG. If the fiber diameter is comparatively large, it will not be cut even if it is plasticized and melted, and the connecting portion 11 will have a strong net-like structure. In this heat treatment, conventionally known means such as a calender, a hot air heater, an infrared heater, steam heating, or a device for sandwiching and heating a cloth between a pair of endless belts facing each other can be used. Of these, by performing heat treatment with a fluid having a calorific value, it is possible to form a communication hole (indicated by an arrow A in FIG. 1) in the thickness direction of the laminated unit. Furthermore, as a particularly preferred embodiment, a hot-melt nonwoven fabric made of a thermoplastic polyamide resin or an ethylene-vinyl acetate copolymer resin is used, and by adopting a heat treatment with steam, the resin is likely to shrink and cut when wet and hot. Therefore, the cutting can be efficiently performed. Further, when it is necessary to compensate for the strength decrease due to plasticizing and melting of the hot melt nonwoven fabric, a filter material for collecting dust may be added as a support of the hot melt nonwoven fabric forming the outermost layer of the deodorizing filter medium. .

【0017】また、この出願に係る方法発明の他の態様
として、例えば、カレンダーのような、流体加熱以外の
処理方法を採用する場合、離型紙上に脱臭粉粒体を散布
し、この表面にホットメルト不織布を積層し、さらに離
型紙を重ねて熱処理し、順次に積層単位を形成すること
によっても、第一発明に係る脱臭濾材を得ることが出来
る。
As another aspect of the method invention according to this application, when a treatment method other than fluid heating, such as calendering, is adopted, deodorant powder granules are sprinkled on the release paper and the surface thereof is sprayed. The deodorizing filter medium according to the first invention can also be obtained by stacking hot-melt nonwoven fabrics, further stacking release paper and heat-treating them to sequentially form laminated units.

【0018】以下、この発明の実施例につき説明する
が、以下に示す実施例は、この発明の理解を容易とする
ための好適例に過ぎず、本願発明はこれら例示条件にの
み限定されるものではない。
Examples of the present invention will be described below, but the following examples are merely preferred examples for facilitating the understanding of the present invention, and the present invention is limited only to these exemplified conditions. is not.

【0019】[0019]

【実施例】始めに、支持体として、ポリエステルからな
る面密度30g/m2のスパンボンドを用い、当該支持
体に熱可塑性ポリアミド系樹脂からなる面密度20g/
2のホットメルト不織布を積層しておく。次いで、こ
のように積層したホットメルト不織布の表面に、分級し
た市販の活性炭(詳細後述)を散布する。続いて、約5
Kg/cm2の水蒸気処理を支持体側(ホットメルト不
織布側)から約7秒間行い、上記ホットメルト不織布を
可塑化溶融して、ホットメルト樹脂からなる連結部と樹
脂凝集部とで構成されたウエブに、樹脂凝集部を介して
活性炭を固着させた。続いて、固着した活性炭以外を除
去することにより、活性炭が、各々の粒径に応じて固着
され、しかも支持体と接着された1層目の積層単位を得
た。さらに、この状態の積層単位に上記ホットメルト不
織布を積層し、活性炭散布、水蒸気処理、並びに固着さ
れていない活性炭の除去を経て2層目、乃至は3層目の
積層単位を形成し、実施例1〜5に係る脱臭濾材を得
た。加えて、熱可塑性ポリアミド系樹脂以外のホットメ
ルト樹脂からなるホットメルト不織布を用いたことを除
いては、実施例2と同一の構成材料を用いて、実施例6
〜10に係る脱臭濾材を作製した。更には、実施例11
として、実施例2で得られた脱臭濾材を、対向する1対
の無端ベルト間に挟持し、温度130℃、圧力0.01
MPaの条件によって10秒間熱圧着した濾材を作製し
た。
Example First, a spunbond having a surface density of 30 g / m 2 made of polyester was used as a support, and a surface density of 20 g / m made of a thermoplastic polyamide resin was used for the support.
Laminate m 2 hot melt non-woven fabric. Then, classified commercial activated carbon (described later in detail) is sprayed on the surface of the hot-melt nonwoven fabric laminated in this way. Then, about 5
A web composed of a connection part made of hot melt resin and a resin agglomeration part is obtained by subjecting the hot melt non-woven fabric to plasticization and melting by subjecting the support side (hot melt non-woven fabric side) to steam treatment of Kg / cm 2 for about 7 seconds. Then, activated carbon was fixed to the resin through the resin aggregating portion. Subsequently, the activated carbon other than the fixed activated carbon was removed to obtain a first-layer laminated unit in which the activated carbon was fixed according to each particle size and was bonded to the support. Further, the hot melt non-woven fabric was laminated on the lamination unit in this state, and the second layer or the third layer of the lamination unit was formed through activated carbon spraying, steam treatment, and removal of unfixed activated carbon. A deodorizing filter material according to 1 to 5 was obtained. In addition, the same constituent materials as in Example 2 were used, except that a hot-melt nonwoven fabric made of a hot-melt resin other than the thermoplastic polyamide resin was used.
Deodorizing filter media according to Nos. 10 to 10 were produced. Furthermore, Example 11
The deodorizing filter material obtained in Example 2 was sandwiched between a pair of opposed endless belts, and the temperature was 130 ° C. and the pressure was 0.01.
A filter medium was prepared by thermocompression bonding for 10 seconds under the condition of MPa.

【0020】また、比較のため、平均粒径0.375m
mの活性炭100重量部に対して、ポリアミド系の粒状
接着剤である「ベスタメルト430P2」(ダイセルヒ
ュルス(株)製、商品名:平均粒径0.16mm)25
重量部を乾燥状態で混合し、これら混合物を前述のポリ
エステルスパンボンドを支持体として塗布形成後、15
0℃で5分間加熱することにより、活性炭同士が上記接
着剤で点接着された比較例に係る脱臭濾材を作製した。
これら実施例1〜11、並びに比較例に係る各々の濾材
の詳細を表1、圧力損失の測定結果、脱臭効率の測定結
果及び加工性の評価結果を表2に、各々示す。
For comparison, the average particle size is 0.375 m.
“VESTAMELT 430P2” (manufactured by Daicel Hüls KK, trade name: average particle size 0.16 mm), which is a polyamide-based granular adhesive, per 100 parts by weight of m of activated carbon 25
15 parts by weight are mixed in a dry state, and the mixture is coated and formed with the above polyester spunbond as a support.
By heating at 0 ° C. for 5 minutes, a deodorizing filter medium according to a comparative example in which activated carbons were spot-bonded to each other with the above adhesive was produced.
Table 1 shows the details of the filter media according to Examples 1 to 11 and Comparative Example, and Table 2 shows the pressure loss measurement results, the deodorization efficiency measurement results, and the processability evaluation results.

【0021】[0021]

【表1】 [Table 1]

【0022】[0022]

【表2】 [Table 2]

【0023】以下、脱臭性能の測定方法に付き説明す
る。まず、圧力損失の測定に当たっては、定法に従い、
各々の脱臭濾材に10cm/秒の風速で送風し、濾材の
上下流での圧力の差を求めた。その結果、粒状接着剤で
構成した比較例と実施例5との比較から明らかなよう
に、この発明を適用した濾材では、実質的に同量、同一
平均粒径の脱臭粉粒体で構成したにも関わらず、圧力損
失は比較例に較べて約2/3と顕著な効果が認められ
た。また、実施例1〜11に係る本発明適用の濾材で
は、何れも低圧損であることが理解できる。さらに、当
該比較例に係る濾材を肉眼で観察したところ、濾材の支
持体側の面に、粒状接着剤に起因すると考えられるフィ
ルム状の部分が点在して認められた。
The method of measuring the deodorizing performance will be described below. First, in measuring pressure loss, according to the standard method,
Air was blown to each of the deodorizing filter media at a wind speed of 10 cm / sec, and the pressure difference between the upstream and downstream sides of the filter media was determined. As a result, as is clear from the comparison between the comparative example composed of the granular adhesive and Example 5, the filter medium to which the present invention was applied was composed of deodorized powder particles having substantially the same amount and the same average particle size. Nevertheless, the pressure loss was about ⅔ compared with the comparative example, showing a remarkable effect. Further, it can be understood that the filter media of the present invention according to Examples 1 to 11 all have low pressure loss. Further, when the filter medium according to the comparative example was observed with the naked eye, film-like portions which were considered to be caused by the granular adhesive were scattered on the support-side surface of the filter medium.

【0024】脱臭効率の測定は、臭気物質としてトルエ
ンを用い、初期濃度25ppm、風速14cm/秒の条
件で行った。この測定では測定開始から1分後を試験条
件が定常に達したと見なして初期とし、その後、10分
毎に30分迄の測定を行った。結果については、初期濃
度(上流側濃度)と濾材を通過した後の下流側濃度との
差を初期濃度で割り、百分率で求めた。表2から理解で
きるように、実施例5と比較例とから、本発明の適用に
よる構造上の優位性が確認できた。この比較例の濾材を
電子顕微鏡で観察したところ、固着に寄与していない接
着剤と思われる成分によって、一部の活性炭表面が被覆
されていた。また、実施例1〜10の結果から、脱臭粉
粒体の平均粒径が小さいほど初期特性は良好であった。
加えて、実施例11に係る濾材の脱臭効率測定結果は表
記を省略するが、ほぼ実施例2と同等であり、2つの加
熱手段を経て作製されたことにより厚さの低減(加工性
の向上)を図ることができ、大きな圧力損失の増大は生
じず、優れた脱臭性能を示した。
The deodorization efficiency was measured by using toluene as an odor substance under the conditions of an initial concentration of 25 ppm and an air velocity of 14 cm / sec. In this measurement, 1 minute after the start of measurement, the test conditions were considered to have reached a steady state, and the measurement was made initial, and thereafter, every 10 minutes, measurement was performed for 30 minutes. Regarding the results, the difference between the initial concentration (upstream concentration) and the downstream concentration after passing through the filter medium was divided by the initial concentration and calculated as a percentage. As can be understood from Table 2, the structural superiority by application of the present invention was confirmed from Example 5 and Comparative Example. When the filter medium of this comparative example was observed with an electron microscope, it was found that a part of the surface of the activated carbon was covered with a component considered to be an adhesive agent that did not contribute to the fixation. Further, from the results of Examples 1 to 10, the smaller the average particle size of the deodorant powder granules, the better the initial characteristics.
In addition, although the deodorization efficiency measurement result of the filter medium according to Example 11 is omitted, it is almost the same as that of Example 2, and the thickness is reduced by being manufactured through two heating means (improved workability. ) Was achieved, a large increase in pressure loss did not occur, and excellent deodorizing performance was exhibited.

【0025】さらに、上述した11種の濾材の夫々につ
いて、90゜の角度で折り加工を行ったところ、実施例
に係る11種の濾材では折られた部分での損傷を実質的
に認めなかったのに対して、比較例に係る濾材では肉眼
で確認できる程度の亀裂を生じ、一部の脱臭粉粒体が脱
落していた。
Further, when each of the 11 kinds of filter media described above was folded at an angle of 90 °, the 11 kinds of filter media according to the examples showed substantially no damage at the folded parts. On the other hand, in the filter medium according to the comparative example, cracks that could be visually confirmed were generated, and a part of the deodorized powder particles had fallen off.

【0026】上述の説明から理解できるように、本発明
を適用した実施例の濾材では、何れも脱臭効率と圧力損
失との双方に優れ、加工性も良好であった。一方、比較
例として挙げた粒状接着剤を用いた技術では、濾材重量
のうち、約19%が接着剤であるのに対して、ほぼ同等
の脱臭粉粒体担持量とした実施例5では、約11%であ
る。このことから、ホットメルト不織布を用いた本発明
に係る技術では、脱臭粉粒体を固着するに当たり、加工
性を損なうことなく脱臭に関与しない構成成分の比率を
最小限に抑え、これによって高い脱臭効率と低い圧力損
失とを実現し得ることが明らかとなった。
As can be understood from the above description, each of the filter media of the examples to which the present invention was applied was excellent in both deodorizing efficiency and pressure loss and had good workability. On the other hand, in the technique using the granular adhesive given as the comparative example, about 19% of the weight of the filter medium is the adhesive, whereas in Example 5 the amount of the deodorized powder granules carried is almost the same, It is about 11%. From this, in the technique according to the present invention using the hot melt nonwoven fabric, in fixing the deodorant powder granules, the ratio of the constituents not involved in deodorization without impairing the processability is minimized, and thereby high deodorization is achieved. It has become clear that efficiency and low pressure drop can be achieved.

【0027】[0027]

【発明の効果】上述した説明からも明らかなように、こ
の出願発明を適用することによって、脱臭粉粒体を連続
した構成成分であるウエブに固着した脱臭濾材を実現す
ることが出来る。従って、脱臭効率が高く、低圧損であ
り、しかも加工性に優れた脱臭濾材を提供することが出
来る。
As is apparent from the above description, by applying the invention of this application, it is possible to realize a deodorizing filter medium in which deodorizing powder particles are fixed to a web which is a continuous constituent. Therefore, it is possible to provide a deodorizing filter medium having high deodorizing efficiency, low pressure loss, and excellent workability.

【図面の簡単な説明】[Brief description of drawings]

【図1】 本発明を説明するため、脱臭濾材の一部を示
す模式的な断面図。
FIG. 1 is a schematic cross-sectional view showing a part of a deodorizing filter medium for explaining the present invention.

【図2】 本発明を説明するため、脱臭濾材の一部を概
略平面で示す図。
FIG. 2 is a diagram schematically showing a part of a deodorizing filter medium for explaining the present invention.

【符号の説明】[Explanation of symbols]

11:連結部 13:樹脂凝集部 1
5:ウエブ 17:脱臭粉粒体 19:積層単位
A:連通孔。
11: Connection part 13: Resin aggregation part 1
5: Web 17: Deodorized powder granules 19: Lamination unit
A: Communication hole.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI B01D 53/81 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI B01D 53/81

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ホットメルト樹脂のみからなる連結部と
樹脂凝集部とで構成されたウエブの一方の表面に、前記
樹脂凝集部を介して脱臭粉粒体を固着してなる積層単位
を有し、前記ウエブの他方の表面と、他の積層単位を構
成する脱臭粉粒体とが樹脂凝集部を介して固着してなる
ことを特徴とする脱臭濾材。
1. A laminated unit in which deodorized powder granules are fixed to one surface of a web composed of a connecting part made of only hot-melt resin and a resin agglomerate part through the resin agglomerate part. A deodorizing filter material, characterized in that the other surface of the web and deodorizing powder particles constituting another laminated unit are adhered to each other via a resin aggregating portion.
【請求項2】 前記ホットメルト樹脂が熱可塑性ポリア
ミド系樹脂、熱可塑性ポリエステル樹脂、熱可塑性ポリ
ウレタン樹脂、ポリオレフィン樹脂またはポリオレフィ
ン変性樹脂からなることを特徴とする請求項1に記載の
脱臭濾材。
2. The deodorizing filter material according to claim 1, wherein the hot melt resin is made of a thermoplastic polyamide resin, a thermoplastic polyester resin, a thermoplastic polyurethane resin, a polyolefin resin or a polyolefin modified resin.
【請求項3】 請求項1に記載のウエブの厚さが、前記
脱臭粉粒体の平均粒径よりも小さいことを特徴とする請
求項1に記載の脱臭濾材。
3. The thickness of the web according to claim 1, wherein
A contract characterized by being smaller than the average particle size of deodorized powder
The deodorizing filter medium according to claim 1.
【請求項4】 ホットメルト不織布の表面に脱臭粉粒体
を配した後、加熱処理によって前記ホットメルト不織布
と前記脱臭粉粒体とが接する部分に樹脂凝集部を形成
し、かつ該樹脂凝集部とホットメルト樹脂からなる連結
部とからなるウエブを形成する第一の工程と、前記脱臭
粉粒体のうち、前記ウエブに固着された脱臭粉粒体のみ
を残存せしめて積層単位を形成する第二の工程と、該積
層単位の前記脱臭粉粒体に接してホットメルト不織布を
積層し、続いて、該ホットメルト不織布の表面に脱臭粉
粒体を配した後、前記第一の工程と前記第二の工程とを
順次行うことを特徴とする脱臭濾材の製造方法。
4. A hot-melt non-woven fabric is provided with deodorant powder granules, and then a heat treatment is performed to form a resin agglomerate at a portion where the hot melt non-woven fabric and the deodorant powder granules are in contact with each other, and the resin agglomerate is formed. And a first step of forming a web consisting of a connecting portion made of hot-melt resin, of the deodorized powder granules, only the deodorized powder granules fixed to the web are left to form a laminated unit Second step, a hot melt nonwoven fabric is laminated in contact with the deodorizing powder granules of the lamination unit, and subsequently, the deodorizing powder granules are arranged on the surface of the hot melt nonwoven fabric, and then the first step and the above A method for producing a deodorizing filter medium, which comprises sequentially performing the second step.
【請求項5】 前記第一の工程における加熱処理を水蒸
気処理としたことを特徴とする請求項に記載の脱臭濾
材の製造方法。
5. The process for producing a deodorizing filter medium according to claim 4, characterized in that the heat treatment in the first step was steamed.
【請求項6】6. 前記ホットメルト不織布の開口径を、前If the opening diameter of the hot melt nonwoven fabric is
記脱臭粉粒体の粒径よりも小さくしたことを特徴とするIt is characterized in that it is made smaller than the particle size of the deodorizing powder granules.
請求項4に記載の脱臭濾材の製造方法。The method for producing the deodorizing filter medium according to claim 4.
JP04621598A 1995-06-03 1998-02-12 Deodorizing filter medium and method for producing the same Expired - Lifetime JP3487754B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP04621598A JP3487754B2 (en) 1998-01-12 1998-02-12 Deodorizing filter medium and method for producing the same
KR10-1998-0020254A KR100477525B1 (en) 1995-06-03 1998-06-01 Multilayer deodorant filter medium and its manufacturing method
EP98110035A EP0882485B1 (en) 1997-06-03 1998-06-02 Laminated deodorant filter medium and method of making the same
US09/088,776 US6177069B1 (en) 1997-06-03 1998-06-02 Laminated deodorant filter medium and method of making the same
DE69807583T DE69807583T2 (en) 1997-06-03 1998-06-02 Laminated deodorization filter medium and manufacturing process

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP1813198 1998-01-12
JP10-18131 1998-01-12
JP04621598A JP3487754B2 (en) 1998-01-12 1998-02-12 Deodorizing filter medium and method for producing the same

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Publication Number Publication Date
JPH11253720A JPH11253720A (en) 1999-09-21
JP3487754B2 true JP3487754B2 (en) 2004-01-19

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Country Link
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KR100337537B1 (en) * 2000-05-31 2002-05-22 김용민 A process of preparing for the composite nonwoven fabric with activated carbon fiber
JP2005246306A (en) * 2004-03-05 2005-09-15 Kanai Hiroaki Cartridge filter for removing ion and manufacturing method therefor
JP2005288429A (en) * 2004-03-11 2005-10-20 Japan Vilene Co Ltd Ozone decomposition material, method for producing ozone decomposition material, method for decomposing ozone, and method for regenerating ozone decomposition material
JP4815138B2 (en) * 2005-03-22 2011-11-16 日本バイリーン株式会社 Flame retardant deodorizing filter media
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JPH11253720A (en) 1999-09-21

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